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    HYDROGEN-ENRICHED FEEDSTOCK FOR FLUIDIZED CATALYTIC CRACKING PROCESS
    64.
    发明申请
    HYDROGEN-ENRICHED FEEDSTOCK FOR FLUIDIZED CATALYTIC CRACKING PROCESS 有权
    氢化催化裂化工艺的氢化进料

    公开(公告)号：US20130026067A1

    公开(公告)日：2013-01-31

    申请号：US13493270

    申请日：2012-06-11

    申请人： Omer Refa KOSEOGLU

    发明人： Omer Refa KOSEOGLU

    IPC分类号： C10G47/00 ,  C10G1/00

    CPC分类号： C10G11/18 ,  C10G45/20 ,  C10G45/22 ,  C10G47/30 ,  C10G49/007 ,  C10G2300/202 ,  C10G2300/207 ,  C10G2400/02

    摘要： A process for catalytically cracking a hydrocarbon oil containing sulfur and/or nitrogen hydrocarbon constituents by dissolving excess hydrogen in the liquid hydrocarbon feedstock in a mixing zone at a temperature of 420° C. to 500° C. and a hydrogen-to-feedstock oil volumetric ratio of 300:1 to 3000:1, flashing the mixture to remove remaining hydrogen and any light components in the feed, introducing the hydrogen saturated hydrocarbon feed into an FCC reactor for contact with a catalyst suspension in a riser or downflow reactor to produce lower boiling hydrocarbon components which can be more efficiently and economically separated into lower molecular weight hydrocarbon products, hydrogen sulfide and ammonia gas and unreacted hydrogen in a separation zone. Hydrogen present in the liquid phase enhances the desulfurization and denitrification reactions which occur during the conversion process and allows for the removal of significantly more sulfur- and/or nitrogen-containing contaminants from the feedstock in an economical fashion.

    摘要翻译： 一种通过在420℃至500℃的温度下将过量的氢溶解在液态烃原料的混合区中，将含硫和/或氮烃成分的烃油催化裂解的方法，以及氢至原料油 体积比为300:1至3000:1，闪蒸混合物以除去进料中的剩余氢气和任何轻组分，将氢饱和烃进料引入FCC反应器中以与提升管或下流式反应器中的催化剂悬浮液接触以产生 较低沸点的烃组分可以更有效和经济地分离成较低分子量的烃产物，硫化氢和氨气以及分离区中的未反应的氢。 存在于液相中的氢增强了在转化过程中发生的脱硫和脱氮反应，并允许以经济的方式从原料中除去显着更多的含硫和/或含氮污染物。

    Integrated Selective Hydrocracking and Fluid Catalytic Cracking Process
    65.
    发明申请
    Integrated Selective Hydrocracking and Fluid Catalytic Cracking Process 审中-公开
    综合选择加氢裂化和流体催化裂化工艺

    公开(公告)号：US20130026065A1

    公开(公告)日：2013-01-31

    申请号：US13558118

    申请日：2012-07-25

    申请人： Omer Refa Koseoglu

    发明人： Omer Refa Koseoglu

    IPC分类号： C10G69/14 ,  C10G69/04 ,  B01J8/00

    CPC分类号： C10G69/02 ,  C10G2300/1096 ,  C10G2300/202 ,  C10G2300/44

    摘要： An integrated process and system for conversion of a heavy crude oil to produce transportation fuels is provided. The process includes separating the hydrocarbon feed into an aromatic-lean fraction and an aromatic-rich fraction. The aromatic-rich fraction is hydrocracked under relatively high pressure to convert at least a portion of refractory aromatic organosulfur and organonitrogen compounds and to produce a hydrocracked product stream. Unconverted bottoms effluent is recycled to the aromatic separation step. The aromatic-lean fraction is cracked in a fluidized catalytic cracking reaction zone to produce a cracked product stream, a light cycle oil stream and a heavy cycle oil stream. In certain embodiments the aromatic-lean fraction can be hydrotreated prior to fluidized catalytic cracking.

    摘要翻译： 提供了一种用于转化重质原油以生产运输燃料的综合过程和系统。 该方法包括将烃进料分离成稀芳烃馏分和富含芳烃的级分。 富含芳烃的级分在相对高的压力下进行加氢裂化，以转化至少一部分难熔芳族有机硫和有机氮化合物，并产生加氢裂化产物流。 未转化的底部流出物被再循环到芳族分离步骤。 芳烃贫馏分在流化催化裂化反应区裂解，产生裂化产物流，轻循环油流和重循环油流。 在某些实施方案中，芳族馏分可在流化催化裂化之前进行加氢处理。

    DELAYED COKING PROCESS UTILIZING ADSORBENT MATERIALS
    66.
    发明申请
    DELAYED COKING PROCESS UTILIZING ADSORBENT MATERIALS 有权
    延迟焦化工艺利用吸附材料

    公开(公告)号：US20130026064A1

    公开(公告)日：2013-01-31

    申请号：US13533431

    申请日：2012-06-26

    申请人： Omer Refa Koseoglu

    发明人： Omer Refa Koseoglu

    IPC分类号： C10B55/00 ,  C10G25/12

    CPC分类号： C10B57/06 ,  C10B55/02 ,  C10G9/005

    摘要： A delayed coking process includes: a. introducing a fresh hydrocarbon feedstock containing undesirable sulfur and/or nitrogen compounds for preheating into the lower portion of a coking unit product fractionator; b. introducing at least a portion of an intermediate fraction derived from the fractionator and at least one adsorbent material that selectively adsorbs sulfur- and/or nitrogen-containing compounds into a mixing zone to form an adsorbent slurry stream; c. discharging a bottoms fraction from the fractionator; d. adding all or a portion of the slurry stream to the bottoms fraction to form a mixed coking unit feedstream; e. heating the mixed feedstream in the coking unit furnace to a predetermined coking temperature; and f. passing the heated mixed feedstream to a drum of the delayed coking to produce a delayed coking product stream while depositing the adsorbent material having adsorbed sulfur and/or nitrogen compounds with the coke in the coking drum.

    摘要翻译： 延迟焦化过程包括：a。 引入含有不希望的硫和/或氮化合物的新鲜烃原料用于预热到焦化装置产品分馏器的下部; b。 引入至少一部分来自分馏器的中间馏分和至少一种选择性地将含硫和/或含氮化合物吸附到混合区中以形成吸附浆料流的吸附剂材料; C。 从分馏器排出塔底馏分; d。 将全部或一部分浆料流加入塔底馏分以形成混合焦化装置进料流; e。 将焦化单元炉中的混合进料流加热到预定的焦化温度; 和f。 将加热的混合进料流通入延迟焦化的滚筒以产生延迟焦化产物流，同时将具有吸附的硫和/或氮化合物的吸附材料与焦炭放置在焦化鼓中。

    IONIC LIQUID DESULFURIZATION PROCESS INCORPORATED IN A CONTACT VESSEL
    69.
    发明申请
    IONIC LIQUID DESULFURIZATION PROCESS INCORPORATED IN A CONTACT VESSEL 有权
    离子液体脱硫工艺合并在联系船上

    公开(公告)号：US20110233112A1

    公开(公告)日：2011-09-29

    申请号：US13071272

    申请日：2011-03-24

    申请人： Omer Refa KOSEOGLU ,  Adnan Al-Hajji

    发明人： Omer Refa KOSEOGLU ,  Adnan Al-Hajji

    IPC分类号： C10G67/04

    CPC分类号： C10G21/06 ,  C10G21/08 ,  C10G21/28 ,  C10G45/00 ,  C10G67/0463 ,  C10G2300/1055 ,  C10G2300/202 ,  C10G2300/207 ,  C10G2300/301 ,  C10G2300/44 ,  C10G2400/04

    摘要： Initial high sulfur levels of a hydrocarbon feedstock are reduced to desired low levels without the need for integration of substantial new equipment or hardware with existing hydroprocessing reactors. Ionic liquids are utilized as organic sulfur extraction agents and are added to and mixed with the hydrocarbon feedstock containing organosulfur compounds downstream of an existing cold separator vessel. The ionic liquid and hydrocarbon mixture is maintained in a contact vessel under conditions which promote the formation of ionic sulfur-containing derivatives that are soluble in the ionic liquid to be formed, thereby enabling extractive removal and separation of the organosulfur compounds from the feedstock.

    摘要翻译： 烃原料的初始高硫含量降低到所需的低水平，而不需要将大量新设备或硬件与现有的加氢处理反应器集成。 离子液体用作有机硫提取剂，并且与现有冷分离器容器下游的含有有机硫化合物的烃原料相加并混合。 离子液体和烃混合物在促进形成可溶于待形成的离子液体中的离子含硫衍生物的条件下保持在接触容器中，从而能够从原料中萃取除去和分离有机硫化合物。

    INTEGRATED HYDROTREATING AND OXIDATIVE DESULFURIZATION PROCESS
    70.
    发明申请
    INTEGRATED HYDROTREATING AND OXIDATIVE DESULFURIZATION PROCESS 有权
    一体化加氢和氧化脱硫工艺

    公开(公告)号：US20110233110A1

    公开(公告)日：2011-09-29

    申请号：US12748888

    申请日：2010-03-29

    申请人： Omer Refa Koseoglu ,  Abdennour Bourane

    发明人： Omer Refa Koseoglu ,  Abdennour Bourane

    IPC分类号： C10G69/02

    CPC分类号： C10G67/12 ,  B01J8/00 ,  C10G27/00 ,  C10G27/04 ,  C10G31/08 ,  C10G45/02 ,  C10G2300/1055 ,  C10G2300/202 ,  C10G2300/207 ,  C10G2300/44 ,  C10G2400/04

    摘要： A system and process for desulfurizing a hydrocarbon feed stream containing organosulfur compounds is provided. In general, the system includes a conventional hydrotreating unit through the high pressure cold or hot separator. Aqueous oxidant and an oxidative catalyst are mixed with the hydrotreated hydrocarbon effluent from the high pressure cold or hot separator, and oxidative desulfurization reactions occur in the low pressure separation zone, thereby minimizing or eliminating the requirement of additional oxidative desulfurization reactors.

    摘要翻译： 提供了一种用于使含有机硫化合物的烃进料流脱硫的系统和方法。 通常，该系统包括通过高压冷或热分离器的常规加氢处理单元。 将水性氧化剂和氧化催化剂与来自高压冷或热分离器的加氢处理的烃流出物混合，并且氧化脱硫反应发生在低压分离区中，从而最小化或消除了额外的氧化脱硫反应器的需要。